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filingDate 1997-05-23-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bddb2908c6a95f92f0b625f259284777
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ec8450c82432da1b25874fbaefcf20e0
publicationDate 2002-12-11-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CZ-291103-B6
titleOfInvention A method for producing a high molecular weight ethylene / propylene reactor mixture with a wide molecular weight distribution
abstract The process for producing high molecular weight reactors can be based on a high molecular weight ethylene-propylene copolymer and a polypropylene polypropylene having an ethylene content of 0.1 and 2% by weight, MFR (230/5) melt index. 5 dg / min and the weight distribution of M.sub.w.n./M.sub.n.n. in the range of 6 and 20, the first stage copolymer of propylene and ethylene and the polymer of propylene, first to the ethylene ethylene exchange step and the copolymer with a 4 and 20 carbon atom 1-olefin in suspension at temperatures ranging from 30 and 150 degC, 1 and 10 MPa pressures and 30 minutes and 6 hours, respectively, with the organoaluminum catalyst (B) and the organometallic compound ( (C) in the second stage, in the first stage, both the monomer and the suspension medium is a suspension medium, and in the first stage, a high molecular weight ethylene / propylene copolymer with a viscosity of 500 and 1400 ml / g and 20 and 80% in the polymer, and after the second stage, the polymer has a viscosity of 200 and 400 ml / g and a polydispersity of M.sub.wn / M.sub.nn 6 and 20, a ratio of 2.5 to 4 liters of liquid propylene per kg of PP is set in the first stage and the polymerization is carried out at temperatures of 55 and 100 degC, the ratio between 1 and 2.5 l of liquid propylene per kg of PP is set and no ethylene is injected in the second stage. \ T
priorityDate 1996-05-24-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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